WO2023281703A1 - Apparatus for forming inorganic substance from organic substance - Google Patents

Apparatus for forming inorganic substance from organic substance Download PDF

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Publication number
WO2023281703A1
WO2023281703A1 PCT/JP2021/025798 JP2021025798W WO2023281703A1 WO 2023281703 A1 WO2023281703 A1 WO 2023281703A1 JP 2021025798 W JP2021025798 W JP 2021025798W WO 2023281703 A1 WO2023281703 A1 WO 2023281703A1
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organic matter
processing furnace
body case
main body
weight
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PCT/JP2021/025798
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French (fr)
Japanese (ja)
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弘明 太幡
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株式会社Clear Sky
内田 節夫
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Application filed by 株式会社Clear Sky, 内田 節夫 filed Critical 株式会社Clear Sky
Priority to PCT/JP2021/025798 priority Critical patent/WO2023281703A1/en
Priority to CN202180099913.1A priority patent/CN117615861A/en
Publication of WO2023281703A1 publication Critical patent/WO2023281703A1/en

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless

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  • the present invention relates to an apparatus for converting organic matter into mineral matter, and more particularly, organic matter such as industrial waste is treated with magnetized air (only oxygen is a magnetic substance, so hereinafter referred to as oxygen).
  • the present invention relates to an apparatus for low-temperature pyrolysis treatment to mineralize.
  • a low-temperature pyrolysis apparatus is known as a device for low-temperature pyrolysis treatment of organic matter such as industrial waste by the action of magnetized oxygen to make it inorganic.
  • a magnetized fluid supplier 2 for magnetizing the air a processing chamber 6 having a side portion 3 and a bottom portion 5 made of iron, into which dust is introduced and stored, and an upper wall portion 7 provided with a dust inlet 7a. , a lid portion 8 covering the inlet 7a, and a plurality of magnetic fluid feeders 2, which are in communication with each other, and whose tips protrude from the side portion 3 and the bottom portion 5 of the processing chamber 6 toward the interior of the processing chamber 6.
  • a fluid supply pipe section 10 and a gas purifier 11 for purifying air containing harmful substances such as dioxins generated after heat treatment A magnetized fluid supply device 2 that magnetizes air, a processing chamber 6 having a side portion 3 and a bottom portion 5 made of iron, into which dust is introduced and stored, and an upper wall portion 7 provided with a dust inlet 7a. , a lid portion 8 covering the inlet 7a, and a plurality of fluids communicating with the magnetized fluid supply device 2 and projecting from the side portion 3 and the bottom portion 5 of the processing chamber 6 toward the inside of the processing chamber 6. It is provided with a supply pipe section 10 and a gas purifier 11 for purifying air containing harmful substances such as dioxins generated after heat treatment.
  • a low-temperature pyrolysis apparatus is an apparatus for heat-treating an object to be treated by introducing magnetized oxygen.
  • a plurality of fluid supply tube portions communicating with a magnetized fluid supplier and having tips projecting from the side and bottom of the processing chamber toward the interior of the processing chamber; and a gas purifier for purifying air containing harmful substances such as dioxin.
  • Air supply in the processing chamber is natural air supply with unstable supply, which may cause uneven treatment (for example, if the waste is only plastic, it may harden before it is decomposed). .).
  • this type of magnetic treatment apparatus is of the heat conduction type, the organic matter cannot be decomposed unless the organic matters are in close contact with each other. Since the thickness is not too large, gaps are likely to be formed between the organic substances, and there is a risk that heat will not be conducted sufficiently.
  • the mechanism for discharging the ash generated after the heat treatment is a pair of screw feeders arranged side by side, and the ash is easily clogged due to the structure that rotates inward and entangles the ash, causing failure. .
  • An object of the present invention is to provide an apparatus for converting organic substances to inorganic substances, which enables efficient low-temperature pyrolysis treatment because it is carried out satisfactorily, and eliminates the risk of ash clogging a screw feeder for discharging ash.
  • a processing furnace having a V-shaped cross-sectional bottom surface is disposed in a main body case having an inlet on the top surface, and a magnetization box installed in the main body case magnetizes the processing furnace.
  • Organic matter put into the processing furnace is thermally decomposed at a low temperature by supplied air directed into the processing furnace from a large number of magnetized oxygen supply nozzles, and is discharged by the discharge means provided in the center of the V-shaped bottom surface.
  • a device for discharging the ash generated by the thermal decomposition The main body case is provided with means for constantly and forcibly supplying a fixed amount of air into the processing furnace, and a weight is provided in the processing furnace for pressurizing the introduced organic matter,
  • the weight is attached to a pivot shaft through a plurality of support arms, and the pivot shaft is a link pivotally supported at the tip of a cylinder rod of a weight drive cylinder pivotally attached to the outer surface of the main body case. It can be driven to rotate by being fixed to the plate, The weight is lifted above the organic matter deposited on the V-shaped bottom surface by the action of the weight drive cylinder, and then becomes free by removing the air from the weight drive cylinder and rotates downward under its own weight.
  • An apparatus for converting an organic substance to an inorganic substance is characterized by moving and pressurizing the organic substance.
  • the discharge means is a single screw feeder, and the direction of the screw in one half and the direction of the screw in the other half are reversed.
  • a cover is arranged so as to cover the magnetized oxygen supply nozzles arranged in parallel. Also, in one embodiment, the magnetized oxygen supply nozzle is horizontally inclined 11 to 20 degrees counterclockwise from the vertical plane and 6 to 10 degrees downward from the horizontal plane.
  • the inlet is provided with a lower inner door that is located below the outer door and opens and closes by cylinder drive to temporarily receive the introduced organic matter.
  • a door for operating a breaking rod for breaking down organic matter in the processing furnace is provided so as to pass from the side wall of the main body case to the side wall of the processing furnace.
  • the processing furnace is provided with a reflux window for discharging unnecessary air after use.
  • the apparatus for converting organic matter into mineral matter since the supply of air to the processing chamber is constantly and forcibly supplied at a constant rate, uneven treatment does not occur, and the introduced organic matter is pressurized by the weight. As a result, there are no gaps between the organic substances, so that heat conduction is performed well, so that efficient low-temperature pyrolysis treatment is possible. Furthermore, the screw feeder for discharging the ash is uniaxial, and the direction of the screw in one half is opposite to the direction of the screw in the other half, so the ash can be discharged smoothly without clogging. It has the effect of being possible.
  • FIG. 1 is a front view showing the configuration of an apparatus for converting organic matter to mineral matter according to the present invention
  • FIG. FIG. 2 is a right side view showing the configuration of the apparatus for converting organic matter to mineral matter according to the present invention
  • 1 is a left side view showing the configuration of an apparatus for converting organic matter into inorganic matter according to the present invention
  • FIG. 1 is a view showing the internal configuration of a processing furnace of an apparatus for converting organic matter to inorganic matter according to the present invention
  • FIG. FIG. 2 is a plan view showing the configuration of the discharge section of the apparatus for converting organic matter to inorganic matter according to the present invention
  • 1 is a longitudinal sectional view showing the configuration of a discharge section of an apparatus for converting organic matter to mineral matter according to the present invention
  • FIG. FIG. 2 is a front view and a side view showing the structure of a weight in the apparatus for converting organic matter into inorganic matter according to the present invention;
  • An apparatus for converting organic matter to inorganic matter is an apparatus for treating organic matter by pyrolysis, which does not require fuel, to make inorganic matter.
  • a processing furnace 11 having a V-shaped bottom surface 12 in cross section is arranged in a main body case 1 having a port 2 . Further, the body case 1 is provided with a gas purifier 3 for purifying the air containing harmful substances such as dioxins generated after the heat treatment.
  • the gas purifier 3 plays a role of taking in the treated air from the treatment furnace 11 and discharging it into the atmosphere after the purification treatment.
  • a magnetization box 21 is further installed in the main body case 1 , and magnetized oxygen is supplied from a large number of magnetized oxygen supply nozzles 22 projecting into the processing furnace 11 . is thermally decomposed at a low temperature, and the ash generated by the thermal decomposition is discharged by the discharge means 31 provided in the central portion of the V-shaped bottom surface 12 .
  • an air pump (not shown) is provided outside the main body case 1 for constantly forcibly supplying a fixed amount of air into the processing furnace 11 .
  • Air is supplied from the air pump to each magnetization box 21 via, for example, a valve and a pressure reducing valve provided inside the gas purifier 3 . Then, the oxygen magnetized in the magnetization box 21 is constantly supplied into the processing furnace 11 from the magnetized oxygen supply nozzle 22 .
  • the reason why the air pump, which is a means of constantly supplying fixed amount of air, is constantly supplied with fixed amount of air is mainly to reduce unevenness in processing speed, thereby avoiding the problem of hardening of plastic waste. be. This is also to suppress backflow to the magnetized oxygen supply nozzle 22 that occurs when the ash outlet 34 or the inlet 2 is closed after the ash outlet 34 or the inlet 2 is open for a long time and the internal temperature rises. .
  • an air compressor (not shown) for supplying compressed air to a door opening/closing cylinder 7 and a weight driving cylinder 43, which will be described later, is installed outside the main body case 1. As shown in FIG.
  • the inlet 2 is covered with a substantially triple-structured lid.
  • the lid is located under the outer door 4, the upper inner door 5 arranged adjacent to it, and the upper inner door 5, and is opened and closed by the cylinder drive, and the lower side that temporarily receives the introduced organic matter. It consists of three lids for the inner door 6 (see Figure 2).
  • the outer door 4 and the upper inner door 5 are manually operated, and the lower inner door 6 is mechanically driven by a door opening/closing cylinder 7. ⁇ A damper 10 is attached to the outer door 4 .
  • the lower inner door 6 is a pair of double doors, which are driven by a pair of door opening/closing cylinders 7 from a horizontal closed state (see FIG. 2) to rotate downward to an open state (see FIG. 3). Let the organic matter fall.
  • the door opening/closing cylinder 7 is installed with its lower end pivotally attached to the outer surface of the main body case 1, and the tip of the cylinder rod is connected to a rotating shaft 8 extending along the long side of the lower inner door 6. It is pivotally attached to a link plate 9 fixed to the end (see FIGS. 1 and 3). In such a configuration, the lower inner door 6 is opened and closed by rotating the link plate 9 and the rotating shaft 8 integrally with the expansion and contraction of the cylinder rod.
  • a weight 41 for pressurizing the organic matter introduced into the processing furnace 11 is installed in the main body case 1 (Figs. 1 to 3, 7).
  • the weight 41 in the illustrated example is attached to a rotating shaft 42 via a plurality of support arms 41a, and both ends of the rotating shaft 42 are supported by bearings installed on both side walls of the body case 1. are arranged in the processing furnace 11.
  • a pair of left and right weights 41 having such a configuration are arranged in FIGS.
  • the tip of the cylinder rod of the weight drive cylinder 43 is pivotally attached to the link plate 44 fixed to the rotation shaft 42 of the weight 41, as in the case of the lower inner door 6 described above.
  • the weight 41 is lifted to a horizontal position by the action of the weight driving cylinder 43, and then released by removing the air from the weight driving cylinder 43, so that it rotates downward under its own weight (see FIG. 2). ), the organic matter deposited on the V-shaped bottom surface 12 is pressurized by its own weight. As a result, there are no gaps between the organic substances, and the organic substances are brought into close contact with each other, so that heat is sufficiently conducted as a whole. Further, from the movement of this weight 41, the processing speed can be grasped. In other words, when the weight 41 is slow to decrease, it can be determined that the processing speed is slow.
  • the basic configuration of the magnetization box 21 installed on the outer wall of the main body case 1 and the principle of air magnetization are not particularly different from those in the conventional device, for example, the invention of Patent Document 1, so detailed description is omitted. do.
  • the magnetized oxygen in the magnetization box 21 is supplied to each of the magnetized oxygen supply nozzles 22, which are installed in the lower part of the processing furnace 11 and directed inward, through a flexible hose 23 made of stainless steel or the like extending from the magnetization box 21. sent (see FIG. 4). As many flexible hoses 23 as the number of magnetized oxygen supply nozzles 22 are prepared, they are converged at appropriate points for better fitting.
  • the magnetized oxygen supply nozzle 22 is preferably installed at a horizontal angle of 11 to 20 degrees and a downward vertical angle of 6 to 10 degrees.
  • the reason why the horizontal angle is set to 11 to 20 degrees is that the magnetic current in the processing furnace 11 normally circulates spirally, and this circulation is promoted more.
  • the reason why the vertical angle is set to 6 to 10 degrees is to prevent reverse flow in the magnetized oxygen supply nozzle 22 .
  • a cover plate 24 covering the plurality of magnetized oxygen supply nozzles 22 arranged in parallel is provided for each nozzle row.
  • the discharging means 31 installed at the bottom of the V-shaped bottom surface 12 of the processing furnace 11 has the problem of the conventional twin-screw discharging means, that is, a pair of screw feeders rotate inwardly to each other and entangle the ash. It is a uniaxial screw feeder 31 in which the direction of the screw 32 in one half and the direction of the screw 33 in the other half are opposite. It is characterized by Due to this configuration, the direction of ejection by the screw 32 and the direction of ejection by the screw 33 are opposite (outward). Along with this, the ash outlets 34 are arranged on both side surfaces of the main body case 1 .
  • a plurality of operation doors 51 for breaking down the organic matter in the processing furnace 11 are provided so as to pass from the side wall of the main body case 1 to the side wall of the processing furnace 11 .
  • This is done by opening the operation door 51 and inserting a breaking bar to break down the deposited organic matter.
  • the processing furnace 11 is provided with a reflux window 52 for exhausting unnecessary air after use due to heat rise. The air coming out of the recirculation window 52 passes through the gap between the processing furnace 11 and the main body case 1 and is discharged to the outside.
  • organic matter such as waste to be mineralized is put into the inlet 2 by opening the outer door 4 and the upper inner door 5, and deposited once on the closed lower inner door 6.
  • the lower inner door 6 is opened to drop the organic matter to the bottom of the processing furnace 11, and the lower inner door 6 is closed again. Since the apparatus according to the present invention is of a heat-conducting type, if the organic substances are not in close contact with each other, the heat cannot be conducted and the organic substances cannot be decomposed. The organic substances are brought into close contact with each other in the processing furnace 11 .
  • Magnetic oxygen is continuously supplied to the bottom of the processing furnace 11 from a large number of magnetized oxygen supply nozzles 22 connected to a flexible hose 23 made of stainless steel or the like extending from a magnetization box 21, so that the oxygen in the processing furnace 11 is magnetic. become. That is, the interior of the processing furnace 11 is negatively ionized, and the water in the air and organic matter is weakly electrolyzed by the magnetic force and dissociated into hydrogen ions and hydroxide ions. When the ions with magnetic energy collide with the carbon molecules of the organic matter, heat is generated, and thermal decomposition occurs in an oxygen-free state.
  • the flow of processing in the apparatus for converting organic matter to inorganic matter according to the present invention is the same as in the conventional apparatus. That is, a step of introducing the organic matter to be treated into the processing furnace 11, a step of introducing a fire source into the processing furnace 11, an oxygen magnetization step of introducing air into the magnetization box 21 to magnetize oxygen, and magnetizing the magnetized oxygen.
  • the process of supplying magnetized oxygen from the oxygen supply nozzle 22 into the processing furnace 11, the process of discharging the exhaust gas generated by the heat treatment to the outside via the gas purifier 3, and the process of discharging ash by the screw feeder 31. include.
  • the apparatus for converting organic matter to mineral matter according to the present invention is as described above. Since the supply of air in the treatment furnace 11 is constantly forced to supply a constant amount, uneven treatment does not occur, and the weight 41 adds the charged organic matter. Since no gaps are formed between the organic substances by being pressed, heat conduction is performed well, so that efficient low-temperature pyrolysis treatment is possible. Further, the screw feeder 31 for discharging ash is uniaxial, and the direction of the screw 32 in one half and the direction of the screw 33 in the other half are opposite, so the ash is clogged. It has an effect that it can be discharged smoothly without any trouble, and its industrial applicability is extremely large.

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

[Problem] To provide an apparatus for forming an inorganic substance from an organic substance, which makes it possible to perform efficient low-temperature thermal decomposition treatment because thermal conduction is well performed, and which has no risk of ash being clogged in a screw feeder for discharging ash. [Solution] This apparatus comprises a processing furnace 11 having a V-shaped bottom surface 12 which is disposed in a main body case 1 having an inlet 2 on the upper surface thereof, wherein: air magnetized by a magnetization box 21 installed in the main body case 1 is supplied from a number of magnetization oxygen supply nozzles 22 directed towards the inside of the processing furnace 11, and thereby the organic substance injected into the processing furnace 11 is thermally decomposed at low temperatures; ash generated by thermal decomposition is discharged by a discharge means 31 disposed in the center part of the V-shaped bottom surface 12; and a constant quantity forced air supply means for supplying air into the processing furnace 11 is installed in the main body case 1.

Description

有機物の無機物化装置Apparatus for converting organic matter to inorganic matter
　本発明は、有機物の無機物化装置に関するものであり、より詳細には、産業廃棄物等の有機物を、磁気化した空気（酸素のみが磁性体であるので、以下酸素とする。）の作用で低温熱分解処理して無機物化するための装置に関するものである。 The present invention relates to an apparatus for converting organic matter into mineral matter, and more particularly, organic matter such as industrial waste is treated with magnetized air (only oxygen is a magnetic substance, so hereinafter referred to as oxygen). The present invention relates to an apparatus for low-temperature pyrolysis treatment to mineralize.
　産業廃棄物等の有機物を、磁気化した酸素の作用で低温熱分解処理して無機物化するための装置としては、特許第４４８６６７１号の発明に係る低温熱分解装置が知られている。この空気を磁化する磁化流体供給機２と、鉄製の側部３及び底部５を有し、ゴミが投入されて貯留される処理室６と、ゴミの投入口７ａが設けられた上壁部７と、投入口７ａを覆う蓋部８と、磁化流体供給機２と連通されるとともに、先端が処理室６の側部３及び底部５から処理室６内部に向かって突出して配された複数の流体供給管部１０と、熱処理後に生じたダイオキシン等の有害物質含む空気を浄化するための気体浄化機１１と、を備えている。空気を磁化する磁化流体供給機２と、鉄製の側部３及び底部５を有し、ゴミが投入されて貯留される処理室６と、ゴミの投入口７ａが設けられた上壁部７と、投入口７ａを覆う蓋部８と、磁化流体供給機２と連通されるとともに、先端が処理室６の側部３及び底部５から処理室６内部に向かって突出して配された複数の流体供給管部１０と、熱処理後に生じたダイオキシン等の有害物質を含む空気を浄化するための気体浄化機１１と、を備えている。低温熱分解装置は、磁化された酸素を導入して処理対象物を熱処理するための装置であって、空気を磁化する磁化流体供給機と、ゴミが投入されて貯留される処理室と、蓋部を有する投入口と、磁化流体供給機と連通されると共に、先端が処理室の側部及び底部から処理室内部に向かって突出して配された複数の流体供給管部と、熱処理後に生じたダイオキシン等の有害物質を含む空気を浄化するための気体浄化機とを備えて成るものである。 A low-temperature pyrolysis apparatus according to the invention of Japanese Patent No. 4486671 is known as a device for low-temperature pyrolysis treatment of organic matter such as industrial waste by the action of magnetized oxygen to make it inorganic. A magnetized fluid supplier 2 for magnetizing the air, a processing chamber 6 having a side portion 3 and a bottom portion 5 made of iron, into which dust is introduced and stored, and an upper wall portion 7 provided with a dust inlet 7a. , a lid portion 8 covering the inlet 7a, and a plurality of magnetic fluid feeders 2, which are in communication with each other, and whose tips protrude from the side portion 3 and the bottom portion 5 of the processing chamber 6 toward the interior of the processing chamber 6. It is provided with a fluid supply pipe section 10 and a gas purifier 11 for purifying air containing harmful substances such as dioxins generated after heat treatment. A magnetized fluid supply device 2 that magnetizes air, a processing chamber 6 having a side portion 3 and a bottom portion 5 made of iron, into which dust is introduced and stored, and an upper wall portion 7 provided with a dust inlet 7a. , a lid portion 8 covering the inlet 7a, and a plurality of fluids communicating with the magnetized fluid supply device 2 and projecting from the side portion 3 and the bottom portion 5 of the processing chamber 6 toward the inside of the processing chamber 6. It is provided with a supply pipe section 10 and a gas purifier 11 for purifying air containing harmful substances such as dioxins generated after heat treatment. A low-temperature pyrolysis apparatus is an apparatus for heat-treating an object to be treated by introducing magnetized oxygen. a plurality of fluid supply tube portions communicating with a magnetized fluid supplier and having tips projecting from the side and bottom of the processing chamber toward the interior of the processing chamber; and a gas purifier for purifying air containing harmful substances such as dioxin.
特許第４４８６６７１号公報Japanese Patent No. 4486671
　上記磁気処理装置の場合、以下のような問題がある。
１) 処理室内の給気が、供給量が不安定な自然給気のため、処理ムラが起こるおそれがある（例えば、廃棄物がプラスチック類のみの場合、分解前に硬化してしまうおそれがある。）。
２) この種磁気処理装置は熱伝導型であるため、有機物同士が密着していないと熱が伝わらずに分解できないが、上記磁気処理装置の場合は、有機物は単に投入口から投入されるに過ぎないため、有機物間に隙間ができやすく、十分に熱伝導が行われないおそれがある。
３) 熱処理後に生じた灰を排出するための機構が一対の並設されたスクリューフィーダーであって、互いに内向きに回転して灰を巻き込む構成のために灰が詰まりやすく、故障の原因となる。 The above magnetic processing apparatus has the following problems.
1) Air supply in the processing chamber is natural air supply with unstable supply, which may cause uneven treatment (for example, if the waste is only plastic, it may harden before it is decomposed). .).
2) Since this type of magnetic treatment apparatus is of the heat conduction type, the organic matter cannot be decomposed unless the organic matters are in close contact with each other. Since the thickness is not too large, gaps are likely to be formed between the organic substances, and there is a risk that heat will not be conducted sufficiently.
3) The mechanism for discharging the ash generated after the heat treatment is a pair of screw feeders arranged side by side, and the ash is easily clogged due to the structure that rotates inward and entangles the ash, causing failure. .
　本発明は、従来技術におけるこのような問題をすべて解決するためになされたもので、処理室内の給気が定量強制給気のために処理ムラが起こらず、投入された有機物間における熱伝導が良好に行われるために効率のよい低温熱分解処理が可能であり、また、灰を排出するスクリューフィーダーに灰が詰まるおそれがない有機物の無機物化装置を提供することを課題とする。 The present invention has been devised to solve all such problems in the prior art. Because the air supplied into the processing chamber is forcibly supplied at a constant rate, uneven processing does not occur, and heat conduction between the charged organic substances is improved. An object of the present invention is to provide an apparatus for converting organic substances to inorganic substances, which enables efficient low-temperature pyrolysis treatment because it is carried out satisfactorily, and eliminates the risk of ash clogging a screw feeder for discharging ash.
　上記課題を解決するための請求項１に記載の発明は、上面に投入口を有する本体ケース内に断面Ｖ型底面を有する処理炉が配備され、前記本体ケースに設置された磁化ボックスによって磁化された空気が前記処理炉内に向かう多数の磁化酸素供給ノズルから供給されることにより前記処理炉内に投入された有機物が低温熱分解され、前記Ｖ型底面の中央部に配備された排出手段によって前記熱分解により生じた灰が排出される装置であって、
　前記本体ケースに、前記処理炉内への常時定量強制給気手段が設置され、また、前記処理炉内に、投入された有機物を加圧するウエイトが設置されて成り、
　前記ウエイトは、複数の支持アームを介して回動軸に取り付けられ、前記回動軸は、前記本体ケースの外側面に枢着されたウエイト駆動シリンダーのシリンダーロッドの先端部に枢支されたリンク板に固定されることにより回動駆動可能であり、
　前記ウエイトは、前記ウエイト駆動シリンダーの作用で前記Ｖ型底面上に堆積している有機物の上方に引き上げられ、その後前記ウエイト駆動シリンダーのエアが抜かれることでフリーの状態となり、自重で下方に回動して前記有機物を加圧することを特徴とする有機物の無機物化装置である。 According to the first aspect of the invention for solving the above-mentioned problems, a processing furnace having a V-shaped cross-sectional bottom surface is disposed in a main body case having an inlet on the top surface, and a magnetization box installed in the main body case magnetizes the processing furnace. Organic matter put into the processing furnace is thermally decomposed at a low temperature by supplied air directed into the processing furnace from a large number of magnetized oxygen supply nozzles, and is discharged by the discharge means provided in the center of the V-shaped bottom surface. A device for discharging the ash generated by the thermal decomposition,
The main body case is provided with means for constantly and forcibly supplying a fixed amount of air into the processing furnace, and a weight is provided in the processing furnace for pressurizing the introduced organic matter,
The weight is attached to a pivot shaft through a plurality of support arms, and the pivot shaft is a link pivotally supported at the tip of a cylinder rod of a weight drive cylinder pivotally attached to the outer surface of the main body case. It can be driven to rotate by being fixed to the plate,
The weight is lifted above the organic matter deposited on the V-shaped bottom surface by the action of the weight drive cylinder, and then becomes free by removing the air from the weight drive cylinder and rotates downward under its own weight. An apparatus for converting an organic substance to an inorganic substance is characterized by moving and pressurizing the organic substance.
　一実施形態においては、前記排出手段は１軸のスクリューフィーダーであって、その一半部のスクリューの向きと他半部のスクリューの向きが逆にされる。 In one embodiment, the discharge means is a single screw feeder, and the direction of the screw in one half and the direction of the screw in the other half are reversed.
　一実施形態においては、多数並設される前記磁化酸素供給ノズルを覆うようにカバーが配設される。また、一実施形態においては、前記磁化酸素供給ノズルは、垂直面から水平に１１～２０度反時計回りに傾斜させ、また、水平面から６～１０度下向きに傾斜させて設置される。 In one embodiment, a cover is arranged so as to cover the magnetized oxygen supply nozzles arranged in parallel. Also, in one embodiment, the magnetized oxygen supply nozzle is horizontally inclined 11 to 20 degrees counterclockwise from the vertical plane and 6 to 10 degrees downward from the horizontal plane.
　一実施形態においては、前記投入口には、外扉の下側に位置してシリンダー駆動により開閉し、投入された有機物を一時的に受け止める下側内扉が設置される。 In one embodiment, the inlet is provided with a lower inner door that is located below the outer door and opens and closes by cylinder drive to temporarily receive the introduced organic matter.
　前記本体ケースの側壁から前記処理炉の側壁を抜けるように、前記処理炉内の有機物を突き崩す突き崩し棒の操作用扉が設けられる。 A door for operating a breaking rod for breaking down organic matter in the processing furnace is provided so as to pass from the side wall of the main body case to the side wall of the processing furnace.
　一実施形態においては、前記処理炉に、使用後の不要空気の排出を行なうための還流用窓が形成される。 In one embodiment, the processing furnace is provided with a reflux window for discharging unnecessary air after use.
　本発明に係る有機物の無機物化装置は上記のとおりであって、処理室内の給気が常時定量強制給気とされるために処理ムラが起こらず、投入された有機物がウエイトにより加圧されることにより有機物間に隙間ができないために熱伝導が良好に行われ、以て、効率のよい低温熱分解処理が可能であり、また、このウエイトの動きから処理状況を把握して対処することが可能であり、更に、灰を排出するスクリューフィーダーが一軸であって、一半部のスクリューの向きと他半部のスクリューの向きが逆であるため、灰を詰まらせることなくスムーズに排出することが可能といった効果がある。 In the apparatus for converting organic matter into mineral matter according to the present invention, as described above, since the supply of air to the processing chamber is constantly and forcibly supplied at a constant rate, uneven treatment does not occur, and the introduced organic matter is pressurized by the weight. As a result, there are no gaps between the organic substances, so that heat conduction is performed well, so that efficient low-temperature pyrolysis treatment is possible. Furthermore, the screw feeder for discharging the ash is uniaxial, and the direction of the screw in one half is opposite to the direction of the screw in the other half, so the ash can be discharged smoothly without clogging. It has the effect of being possible.
本発明に係る有機物の無機物化装置の構成を示す正面図である。1 is a front view showing the configuration of an apparatus for converting organic matter to mineral matter according to the present invention; FIG. 本発明に係る有機物の無機物化装置の構成を示す右側面図である。FIG. 2 is a right side view showing the configuration of the apparatus for converting organic matter to mineral matter according to the present invention; 本発明に係る有機物の無機物化装置の構成を示す左側面図である。1 is a left side view showing the configuration of an apparatus for converting organic matter into inorganic matter according to the present invention; FIG. 本発明に係る有機物の無機物化装置の処理炉の内部構成を示す図である。1 is a view showing the internal configuration of a processing furnace of an apparatus for converting organic matter to inorganic matter according to the present invention; FIG. 本発明に係る有機物の無機物化装置の排出部の構成を示す平面図である。FIG. 2 is a plan view showing the configuration of the discharge section of the apparatus for converting organic matter to inorganic matter according to the present invention; 本発明に係る有機物の無機物化装置の排出部の構成を示す縦断面図である。1 is a longitudinal sectional view showing the configuration of a discharge section of an apparatus for converting organic matter to mineral matter according to the present invention; FIG. 本発明に係る有機物の無機物化装置におけるウエイトの構成を示す正面図及び側面図である。FIG. 2 is a front view and a side view showing the structure of a weight in the apparatus for converting organic matter into inorganic matter according to the present invention;
　本発明の実施の形態について、添付図面を参照しつつ詳細に説明する。熱処理が必要とされる産業廃棄物等の有機物を燃焼により処理する場合、有機物は、十分な酸素（空気）の供給の下に炎を出しながら完全燃焼して灰になるが、熱分解の場合、有機物は最低限の酸素（空気）の存在下で乾燥分解し、炎を出さずに蒸し焼き状態で灰になり、処理された  灰の容積は、有機物の約３００分の１から４００分の１に減容される。 Embodiments of the present invention will be described in detail with reference to the accompanying drawings. When organic matter such as industrial waste that requires heat treatment is treated by combustion, the organic matter burns completely with a flame under the supply of sufficient oxygen (air) and becomes ash. , the organic matter decomposes dryly in the presence of a minimum amount of oxygen (air) and becomes ash in a steamed state without flame, and the volume of the treated ash is about 1/300 to 1/400 of the organic matter. is reduced to
　本発明に係る有機物の無機物化装置は、燃料を必要としない上記熱分解によって有機物を処理して無機物化するための装置であり、この装置は図１～３に示されるように、上面に投入口２を備えた本体ケース１内に、断面Ｖ型底面１２を有する処理炉１１が配備されて構成される。また、本体ケース１には、熱処理後に生じたダイオキシン等の有害物質を含む空気を浄化するための気体浄化機３が付設される。気体浄化機３は、処理炉１１から処理後の空気を取り込み、浄化処理後、大気に排出する役目を果たす。 An apparatus for converting organic matter to inorganic matter according to the present invention is an apparatus for treating organic matter by pyrolysis, which does not require fuel, to make inorganic matter. A processing furnace 11 having a V-shaped bottom surface 12 in cross section is arranged in a main body case 1 having a port 2 . Further, the body case 1 is provided with a gas purifier 3 for purifying the air containing harmful substances such as dioxins generated after the heat treatment. The gas purifier 3 plays a role of taking in the treated air from the treatment furnace 11 and discharging it into the atmosphere after the purification treatment.
　本体ケース１には更に磁化ボックス２１が設置され、そこにおいて磁化された酸素が処理炉１１内に突出する多数の磁化酸素供給ノズル２２から供給され、以て、処理炉１１内に投入された有機物が低温熱分解され、Ｖ型底面１２の中央部に配備された排出手段３１によって熱分解により生じた灰が排出される。 A magnetization box 21 is further installed in the main body case 1 , and magnetized oxygen is supplied from a large number of magnetized oxygen supply nozzles 22 projecting into the processing furnace 11 . is thermally decomposed at a low temperature, and the ash generated by the thermal decomposition is discharged by the discharge means 31 provided in the central portion of the V-shaped bottom surface 12 .
　本発明においては更に、本体ケース１の外側に、処理炉１１内へ常時定量強制送気を行なうためのエアポンプ（図示してない）が配備される。エアポンプから各磁化ボックス２１への送気は、例えば、気体浄化機３内に配備されるバルブ及び減圧弁を介して行なわれる。そして、磁化ボックス２１において磁化された酸素が、磁化酸素供給ノズル２２から処理炉１１内に常時定量供給される。 Further, in the present invention, an air pump (not shown) is provided outside the main body case 1 for constantly forcibly supplying a fixed amount of air into the processing furnace 11 . Air is supplied from the air pump to each magnetization box 21 via, for example, a valve and a pressure reducing valve provided inside the gas purifier 3 . Then, the oxygen magnetized in the magnetization box 21 is constantly supplied into the processing furnace 11 from the magnetized oxygen supply nozzle 22 .
　このように常時定量強制給気手段であるエアポンプを配備して常時定量給気を行うのは、主に、処理速度のムラを少なくすることにより、プラスチック廃棄物の硬化といった問題を回避するためである。また、灰取出し口３４や投入口２を長時間開放して内部温度が上昇した後、灰取出し口３４や投入口２を閉じた際に起こる磁化酸素供給ノズル２２への逆流を抑えるためでもある。更に、本体ケース１の外側に、後述する扉開閉シリンダー７及びウエイト駆動シリンダー４３に圧縮空気を供給するためのエアコンプレッサ（図示してない）が設置される。 The reason why the air pump, which is a means of constantly supplying fixed amount of air, is constantly supplied with fixed amount of air is mainly to reduce unevenness in processing speed, thereby avoiding the problem of hardening of plastic waste. be. This is also to suppress backflow to the magnetized oxygen supply nozzle 22 that occurs when the ash outlet 34 or the inlet 2 is closed after the ash outlet 34 or the inlet 2 is open for a long time and the internal temperature rises. . Furthermore, an air compressor (not shown) for supplying compressed air to a door opening/closing cylinder 7 and a weight driving cylinder 43, which will be described later, is installed outside the main body case 1. As shown in FIG.
　投入口２には、実質的に三重構造の蓋が被せられる。その蓋は、外扉４と、それに近接して配置される上側内扉５と、上側内扉５の下に位置してシリンダー駆動により開閉動作し、投入された有機物を一時的に受け止める下側内扉６の３つの蓋から成る（図２参照）。外扉４と上側内扉５はそれぞれ手動とされ、下側内扉６は扉開閉シリンダー７による機械駆動とされる。外扉４には、ダンパー１０が取り付けられる。 The inlet 2 is covered with a substantially triple-structured lid. The lid is located under the outer door 4, the upper inner door 5 arranged adjacent to it, and the upper inner door 5, and is opened and closed by the cylinder drive, and the lower side that temporarily receives the introduced organic matter. It consists of three lids for the inner door 6 (see Figure 2). The outer door 4 and the upper inner door 5 are manually operated, and the lower inner door 6 is mechanically driven by a door opening/closing cylinder 7.例文帳に追加A damper 10 is attached to the outer door 4 .
　下側内扉６は観音開き式の一対の扉で、水平の閉状態（図２参照）から一対の扉開閉シリンダー７に駆動されて下方に回動して開状態（図３参照）となり、受け止めていた有機物を落下させる。扉開閉シリンダー７は、その下端部が本体ケース１の外側面に枢着されて設置され、そのシリンダーロッドの先端部が、下側内扉６の長尺辺に沿って延びる回動軸８の端部に固定されたリンク板９に枢着される（図１，３参照）。かかる構成において、シリンダーロッドの伸縮動作に伴ってリンク板９及び回動軸８が一体に回動することで、下側内扉６が開閉動作する。 The lower inner door 6 is a pair of double doors, which are driven by a pair of door opening/closing cylinders 7 from a horizontal closed state (see FIG. 2) to rotate downward to an open state (see FIG. 3). Let the organic matter fall. The door opening/closing cylinder 7 is installed with its lower end pivotally attached to the outer surface of the main body case 1, and the tip of the cylinder rod is connected to a rotating shaft 8 extending along the long side of the lower inner door 6. It is pivotally attached to a link plate 9 fixed to the end (see FIGS. 1 and 3). In such a configuration, the lower inner door 6 is opened and closed by rotating the link plate 9 and the rotating shaft 8 integrally with the expansion and contraction of the cylinder rod.
　上記構造の蓋の場合、投入口２から有機物を投入するに当たっては、先ず、下側内扉６を閉じた状態で、手動で外扉４と上側内扉５を開け（図２の仮想線参照）、有機物を投入して閉じている下側内扉６上に落とす。そして、その状態のまま人的操作によって外扉４と上側内扉５を閉じ、次いで扉開閉シリンダー７を始動して下側内扉６を開くことにより、下側内扉６上の有機物を自重で落下させる（図３参照）。このように、有機物を直接落下させることなく、一且下側内扉６で受け止めるようにしたのは、有機物を投入する際に、外気が流入することを抑え、また、処理炉１１内の蒸気が逃げるのを防止するためである。 In the case of the lid of the above structure, when the organic matter is introduced from the inlet 2, first, with the lower inner door 6 closed, the outer door 4 and the upper inner door 5 are manually opened (see the phantom lines in FIG. 2). ), the organic matter is put in and dropped onto the closed lower inner door 6 . In this state, the outer door 4 and the upper inner door 5 are manually closed, and then the door opening/closing cylinder 7 is started to open the lower inner door 6, thereby removing the organic matter on the lower inner door 6 by its own weight. (See Figure 3). In this way, the reason why the organic matter is not dropped directly but is received by the lower inner door 6 is that the inflow of outside air is suppressed when the organic matter is charged, and the steam inside the processing furnace 11 is suppressed. to prevent escape.
　本体ケース１には、処理炉１１内に投入された有機物を加圧するウエイト４１が設置される（図１～３，７)。図示した例におけるウエイト４１は、複数の支持アーム４１ａを介して回動軸４２に取り付けられ、その回動軸４２の両端が、本体ケース１の両側壁に設置された軸受によって軸支されることにより、処理炉１１内に配備される。本発明においては、かかる構成のウエイト４１が、図２、３において左右一対配備され、それぞれ本体ケース１の外側面に枢着により設置されたウエイト駆動シリンダー４３によって回動駆動される。その場合、上記下側内扉６の場合と同様に、ウエイト駆動シリンダー４３のシリンダーロッドの先端部が、ウエイト４１の回動軸４２に固定されたリンク板４４に枢着される。 A weight 41 for pressurizing the organic matter introduced into the processing furnace 11 is installed in the main body case 1 (Figs. 1 to 3, 7). The weight 41 in the illustrated example is attached to a rotating shaft 42 via a plurality of support arms 41a, and both ends of the rotating shaft 42 are supported by bearings installed on both side walls of the body case 1. are arranged in the processing furnace 11. In the present invention, a pair of left and right weights 41 having such a configuration are arranged in FIGS. In that case, the tip of the cylinder rod of the weight drive cylinder 43 is pivotally attached to the link plate 44 fixed to the rotation shaft 42 of the weight 41, as in the case of the lower inner door 6 described above.
　このウエイト４１は、ウエイト駆動シリンダー４３の作用で水平状態に引き上げられた後、ウエイト駆動シリンダー４３のエアを抜くことでフリーの状態にされることにより、自重で下方に回動し（図２参照）、Ｖ型底面１２上に堆積している有機物を自重で加圧する。それにより有機物間の隙間がなくなり、有機物同士が密着して全体的に十分な熱伝導が行なわれることになり、以て、良好な低温熱分解処理が可能となる。更に、このウエイト４１の動きから、処理速度を把握することができる。即ち、ウエイト４１がなかなか下がらないときは、処理速度が遅いと判断することができる。 The weight 41 is lifted to a horizontal position by the action of the weight driving cylinder 43, and then released by removing the air from the weight driving cylinder 43, so that it rotates downward under its own weight (see FIG. 2). ), the organic matter deposited on the V-shaped bottom surface 12 is pressurized by its own weight. As a result, there are no gaps between the organic substances, and the organic substances are brought into close contact with each other, so that heat is sufficiently conducted as a whole. Further, from the movement of this weight 41, the processing speed can be grasped. In other words, when the weight 41 is slow to decrease, it can be determined that the processing speed is slow.
　本体ケース１の外壁に設置される磁化ボックス２１の基本的構成、及び、空気磁化の原理は、従来の装置、例えば、特許文献１の発明におけるものと特に変わりはないので、詳細な説明は省略する。この磁化ボックス２１内において磁化された酸素は、磁化ボックス２１から延びるステンレス等のフレキシブルホース２３を介し、処理炉１１内下部において内方に向くように多数設置されている各磁化酸素供給ノズル２２に送られる（図４参照）。フレキシブルホース２３は磁化酸素供給ノズル２２の数分用意されるので、収まりをよくするために適宜箇所で集束される。 The basic configuration of the magnetization box 21 installed on the outer wall of the main body case 1 and the principle of air magnetization are not particularly different from those in the conventional device, for example, the invention of Patent Document 1, so detailed description is omitted. do. The magnetized oxygen in the magnetization box 21 is supplied to each of the magnetized oxygen supply nozzles 22, which are installed in the lower part of the processing furnace 11 and directed inward, through a flexible hose 23 made of stainless steel or the like extending from the magnetization box 21. sent (see FIG. 4). As many flexible hoses 23 as the number of magnetized oxygen supply nozzles 22 are prepared, they are converged at appropriate points for better fitting.
　磁化酸素供給ノズル２２は、好ましくは、水平角度が１１～２０度で下向き垂直角度が６～１０度となるように設置する。水平角度を１１～２０度にするのは、処理炉１１内の磁気流は通常渦巻き状に還流するが、その還流をより促進するためである。また、垂直角度を６～１０度にするのは、磁化酸素供給ノズル２２内における逆流を防止するためである。 The magnetized oxygen supply nozzle 22 is preferably installed at a horizontal angle of 11 to 20 degrees and a downward vertical angle of 6 to 10 degrees. The reason why the horizontal angle is set to 11 to 20 degrees is that the magnetic current in the processing furnace 11 normally circulates spirally, and this circulation is promoted more. The reason why the vertical angle is set to 6 to 10 degrees is to prevent reverse flow in the magnetized oxygen supply nozzle 22 .
　また、好ましい実施形態においては、多数並設されている複数の磁化酸素供給ノズル２２を覆うカバー板２４が、ノズル列ごとに配設される。このようにカバー板２４を配設してその下側に空間を設けることにより、処理炉１１内上部の渦巻き状の還流と同じ還流が生起される。 Also, in a preferred embodiment, a cover plate 24 covering the plurality of magnetized oxygen supply nozzles 22 arranged in parallel is provided for each nozzle row. By arranging the cover plate 24 in this way and providing a space below it, the same spiral reflux as the spiral reflux in the upper part of the processing furnace 11 is generated.
　処理炉１１のＶ型底面１２の底部に設置される排出手段３１は、従来の２軸式の排出手段における問題点、即ち、一対のスクリューフィーダーが互いに内向きに回転して灰を巻き込む構成のために灰が詰まりやすい、という問題を解消するために創案されたもので、それは１軸のスクリューフィーダー３１であって、その一半部のスクリュー３２の向きと他半部のスクリュー３３の向きが逆であることを特徴とする。かかる構成のため、スクリュー３２による排出方向とスクリュー３３による排出方向は逆（それぞれ外方向）となる。それに伴い、灰取出し口３４は本体ケース１の両側面に配設される。 The discharging means 31 installed at the bottom of the V-shaped bottom surface 12 of the processing furnace 11 has the problem of the conventional twin-screw discharging means, that is, a pair of screw feeders rotate inwardly to each other and entangle the ash. It is a uniaxial screw feeder 31 in which the direction of the screw 32 in one half and the direction of the screw 33 in the other half are opposite. It is characterized by Due to this configuration, the direction of ejection by the screw 32 and the direction of ejection by the screw 33 are opposite (outward). Along with this, the ash outlets 34 are arranged on both side surfaces of the main body case 1 .
　本体ケース１の側壁から処理炉１１の側壁を抜けるように、処理炉１１内の有機物を突き崩すための突き崩し棒の操作用扉５１が複数設けられる。この有機物の突き崩しは、例えば、上述したように、ウエイト４１の下降が遅い湯合に操作用扉５１や灰取出し口３４から目視確認し、堆積している有機物を崩す必要がある場合に、操作用扉５１を開けて突き崩し棒を差し込み、堆積している有機物を突き崩すことにより行なう。また、処理炉１１に、使用後の不要な空気を、熱上昇により排出するための還流用窓５２が設けられる。還流用窓５２から出た空気は、処理炉１１と本体ケース１との間の間隙を通って外部に排出される。 A plurality of operation doors 51 for breaking down the organic matter in the processing furnace 11 are provided so as to pass from the side wall of the main body case 1 to the side wall of the processing furnace 11 . For example, as described above, when it is necessary to visually confirm this breaking down of the organic matter from the operation door 51 or the ash outlet 34 in the bath where the weight 41 is slow to descend, and it is necessary to break down the accumulated organic matter, This is done by opening the operation door 51 and inserting a breaking bar to break down the deposited organic matter. Further, the processing furnace 11 is provided with a reflux window 52 for exhausting unnecessary air after use due to heat rise. The air coming out of the recirculation window 52 passes through the gap between the processing furnace 11 and the main body case 1 and is discharged to the outside.
　上記構成の装置において、無機化する廃棄物等の有機物は、外扉４と上側内扉５を開けて投入口２内に投入し、閉じている下側内扉６の上に一旦堆積させ、外扉４と上側内扉５を閉じた後、下側内扉６を開けて有機物を処理炉１１の底部に落下させ、再び下側内扉６を閉じておく。本発明に係る装置は熱伝導型であるため、有機物同士が密着していないと熱が伝わらずに分解できないため、汚物以外の有機物はすべて、破砕機にかけた後に処理炉１１内に投入し、処理炉１１内において有機物同士が密着し合うようにする。 In the apparatus of the above configuration, organic matter such as waste to be mineralized is put into the inlet 2 by opening the outer door 4 and the upper inner door 5, and deposited once on the closed lower inner door 6. After the outer door 4 and the upper inner door 5 are closed, the lower inner door 6 is opened to drop the organic matter to the bottom of the processing furnace 11, and the lower inner door 6 is closed again. Since the apparatus according to the present invention is of a heat-conducting type, if the organic substances are not in close contact with each other, the heat cannot be conducted and the organic substances cannot be decomposed. The organic substances are brought into close contact with each other in the processing furnace 11 .
　処理炉１１の底部には、磁化ボックス２１から延びるステンレス等のフレキシブルホース２３に接統された多数本の磁化酸素供給ノズル２２から磁気酸素が供給され続けていて、処理炉１１内の酸素が磁気化される。即ち、処理炉１１内がマイナスイオン化された状態となり、空気中や有機物中の水分が、磁力によって弱い電気分解を起こし、水素イオンと水酸イオンに解離する。そして、有機物の炭素分子に磁気エネルギーを持ったイオンが衝突することで熱が発生し、無酸素状態で熱分解が起こる。 Magnetic oxygen is continuously supplied to the bottom of the processing furnace 11 from a large number of magnetized oxygen supply nozzles 22 connected to a flexible hose 23 made of stainless steel or the like extending from a magnetization box 21, so that the oxygen in the processing furnace 11 is magnetic. become. That is, the interior of the processing furnace 11 is negatively ionized, and the water in the air and organic matter is weakly electrolyzed by the magnetic force and dissociated into hydrogen ions and hydroxide ions. When the ions with magnetic energy collide with the carbon molecules of the organic matter, heat is generated, and thermal decomposition occurs in an oxygen-free state.
　本発明に係る有機物の無機物化装置における処理の流れは、従来の装置の場合と変わりがない。即ち、処理すべき有機物の処理炉１１内への投入工程、処理炉１１内への火種投入工程、磁化ボックス２１内へ空気を導入して酸素を磁化する酸素磁化工程、磁化された酸素を磁化酸素供給ノズル２２から処理炉１１内へ供給する磁化酸素供給工程、熱処理によって生じた排ガスの、気体浄化機３を介しての外部排出工程、及び、スクリューフィーダー３１による灰の排出工程の各工程を含む。 The flow of processing in the apparatus for converting organic matter to inorganic matter according to the present invention is the same as in the conventional apparatus. That is, a step of introducing the organic matter to be treated into the processing furnace 11, a step of introducing a fire source into the processing furnace 11, an oxygen magnetization step of introducing air into the magnetization box 21 to magnetize oxygen, and magnetizing the magnetized oxygen. The process of supplying magnetized oxygen from the oxygen supply nozzle 22 into the processing furnace 11, the process of discharging the exhaust gas generated by the heat treatment to the outside via the gas purifier 3, and the process of discharging ash by the screw feeder 31. include.
　本発明に係る有機物の無機物化装置は上記のとおりであって、処理炉１１内の給気が常時定量強制給気とされるために処理ムラが起こらず、投入された有機物がウエイト４１により加圧されることにより有機物間に隙間ができないために熱伝導が良好に行われ、以て、効率のよい低温熱分解処理が可能であり、また、このウエイト４１の動きから処理状況を把握して対処することが可能であり、更に、灰を排出するスクリューフィーダー３１が一軸であって、一半部のスクリュー３２の向きと他半部のスクリュー３３の向きが逆であるために、灰を詰まらせることなくスムーズに排出することが可能といった効果のあるものであり、その産業上の利用可能性は極めて大である。 The apparatus for converting organic matter to mineral matter according to the present invention is as described above. Since the supply of air in the treatment furnace 11 is constantly forced to supply a constant amount, uneven treatment does not occur, and the weight 41 adds the charged organic matter. Since no gaps are formed between the organic substances by being pressed, heat conduction is performed well, so that efficient low-temperature pyrolysis treatment is possible. Further, the screw feeder 31 for discharging ash is uniaxial, and the direction of the screw 32 in one half and the direction of the screw 33 in the other half are opposite, so the ash is clogged. It has an effect that it can be discharged smoothly without any trouble, and its industrial applicability is extremely large.
１　　本体ケース
２　　投入口
３　　気体浄化機
４　　外扉
５　　上側内扉
６　　下側内扉
７　　扉開閉シリンダー
１１　　処理炉
１２　　Ｖ型底面
２１　　磁化ボックス
２２　　磁化酸素供給ノズル
２４　　カバー
３１　　スクリューフィーダー
４１　　ウエイト
４３　　ウエイト駆動シリンダー
５１　　操作用扉
５２　　還流用窓 1 Main body case 2 Input port 3 Gas purifier 4 Outer door 5 Upper inner door 6 Lower inner door 7 Door opening/closing cylinder 11 Processing furnace 12 V-shaped bottom 21 Magnetized box 22 Magnetized oxygen supply nozzle 24 Cover 31 Screw feeder 41 Weight 43 Weight Driving cylinder 51 Operation door 52 Recirculation window

Claims (7)

  1. 　上面に投入口を有する本体ケース内に断面Ｖ型底面を有する処理炉が配備され、前記本体ケースに設置された磁化ボックスによって磁化された空気が前記処理炉内に向かう多数の磁化酸素供給ノズルから供給されることにより前記処理炉内に投入された有機物が低温熱分解され、前記Ｖ型底面の中央部に配備された排出手段によって前記熱分解により生じた灰が排出される装置であって、
    　前記本体ケースに、前記処理炉内への常時定量強制給気手段が設置され、また、前記処理炉内に、投入された有機物を加圧するウエイトが設置されて成り、
    　前記ウエイトは、複数の支持アームを介して回動軸に取り付けられ、前記回動軸は、前記本体ケースの外側面に枢着されたウエイト駆動シリンダーのシリンダーロッドの先端部に枢支されたリンク板に固定されることにより回動駆動可能であり、
    　前記ウエイトは、前記ウエイト駆動シリンダーの作用で前記Ｖ型底面上に堆積している有機物の上方に引き上げられ、その後前記ウエイト駆動シリンダーのエアが抜かれることでフリーの状態となり、自重で下方に回動して前記有機物を加圧することを特徴とする有機物の無機物化装置。     A processing furnace having a V-shaped cross-sectional bottom surface is provided in a main body case having an inlet on the upper surface, and air magnetized by a magnetization box installed in the main body case is directed into the processing furnace from a large number of magnetized oxygen supply nozzles. A device in which the organic matter put into the processing furnace is thermally decomposed at a low temperature by being supplied, and the ash generated by the thermal decomposition is discharged by a discharge means arranged at the center of the V-shaped bottom surface,
    The main body case is provided with means for constantly and forcibly supplying a fixed amount of air into the processing furnace, and a weight is provided in the processing furnace for pressurizing the introduced organic matter,
    The weight is attached to a pivot shaft through a plurality of support arms, and the pivot shaft is a link pivotally supported at the tip of a cylinder rod of a weight drive cylinder pivotally attached to the outer surface of the main body case. It can be driven to rotate by being fixed to the plate,
    The weight is lifted above the organic matter deposited on the V-shaped bottom surface by the action of the weight drive cylinder, and then becomes free by removing the air from the weight drive cylinder and rotates downward under its own weight. 1. An apparatus for converting organic matter to inorganic matter, characterized by moving the organic matter to pressurize the organic matter.
  2. 　前記排出手段は１軸のスクリューフィーダーであって、その一半部のスクリューの向きと他半部のスクリューの向きが逆であることを特徴とする、請求項１に記載の有機物の無機物化装置。 The apparatus for converting organic matter to inorganic matter according to claim 1, wherein the discharge means is a single screw feeder, and the direction of the screw in one half is opposite to the direction of the screw in the other half.
  3. 　多数並設される前記磁化酸素供給ノズルを覆うようにカバーが配設される、請求項１又は２に記載の有機物の無機物化装置。 3. The apparatus for converting organic substances into minerals according to claim 1 or 2, wherein a cover is arranged so as to cover the magnetized oxygen supply nozzles arranged in parallel.
  4. 　前記磁化酸素供給ノズルは、垂直面から水平に１１～２０度反時計回りに傾斜させ、また、水平面から６～１０度下向きに傾斜させて設置される、請求項１乃至３のいずれかに記載の有機物の無機物化装置。 4. The magnetized oxygen supply nozzle according to any one of claims 1 to 3, wherein the magnetized oxygen supply nozzle is horizontally inclined by 11 to 20 degrees counterclockwise from the vertical plane and is installed by being inclined downward by 6 to 10 degrees from the horizontal plane. organic mineralization equipment.
  5. 　前記投入口には、外扉の下側に位置してシリンダー駆動により開閉し、投入された有機物を一時的に受け止める下側内扉が設置される、請求項１乃至４のいずれかに記載の有機物の無機物化装置。 5. The inlet is provided with a lower inner door that is located below the outer door and opens and closes by cylinder drive to temporarily receive the introduced organic matter. Equipment for mineralization of organic matter.
  6. 　前記本体ケースの側壁から前記処理炉の側壁を抜けるように、前記処理炉内の有機物を突き崩す突き崩し棒の操作用扉が設けられる、請求項１乃至５のいずれかに記載の有機物の無機物化装置。 6. The organic and inorganic matter according to claim 1, further comprising an operation door for a breaking rod for breaking down organic matter in said processing furnace so as to pass through the side wall of said processing furnace from the side wall of said main body case. conversion device.
  7. 　前記処理炉に、使用後の不要空気の排出を行なうための還流用窓が形成される、請求項１乃至６のいずれかに記載の有機物の無機物化装置。 7. The apparatus for converting organic matter to inorganic matter according to any one of claims 1 to 6, wherein the processing furnace is provided with a reflux window for discharging unnecessary air after use.
PCT/JP2021/025798 2021-07-08 2021-07-08 Apparatus for forming inorganic substance from organic substance WO2023281703A1 (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005029600A (en) * 2003-07-07 2005-02-03 Yoshimitsu Oshima Apparatus for dry distillation and carbonization treatment of waste and method for dry distillation and carbonization treatment
JP2010075823A (en) * 2008-09-25 2010-04-08 Jiro Terasawa Apparatus for decomposition treatment of organic matter
JP2013010088A (en) * 2011-06-30 2013-01-17 Esujekku:Kk Magnetic decomposition treatment apparatus for organic matter
JP2018108571A (en) * 2016-12-28 2018-07-12 坂本　優蔵 Low-temperature thermal decomposition apparatus for organic matters
JP6905242B1 (en) * 2020-01-30 2021-07-21 弘明 太幡 Inorganicization equipment for organic matter

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005029600A (en) * 2003-07-07 2005-02-03 Yoshimitsu Oshima Apparatus for dry distillation and carbonization treatment of waste and method for dry distillation and carbonization treatment
JP2010075823A (en) * 2008-09-25 2010-04-08 Jiro Terasawa Apparatus for decomposition treatment of organic matter
JP2013010088A (en) * 2011-06-30 2013-01-17 Esujekku:Kk Magnetic decomposition treatment apparatus for organic matter
JP2018108571A (en) * 2016-12-28 2018-07-12 坂本　優蔵 Low-temperature thermal decomposition apparatus for organic matters
JP6905242B1 (en) * 2020-01-30 2021-07-21 弘明 太幡 Inorganicization equipment for organic matter

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